Alkane acetates produced by oxidative esterification of olefins over certain oxide catalysts

ABSTRACT

A process for the production of alkane acetates from olefins in the presence of an oxide catalyst selected from the group of oxides consisting of niobium oxide, iron oxide and bismuth oxide, oxygen and a carboxylate ion source via oxidative esterification is described. The reaction is conducted at a temperature in the range of 100° to 250° C. and a pressure of 1 atmosphere or greater. Iron oxide catalysts are preferred. Alkane diacetates and hydroxy acetates are produced which may be used as precursors to alkylene oxides, alkylene glycols and other useful compounds.

CROSS-REFERENCES TO RELATED APPLICATIONS

This application is related to U.S. patent application Ser. No. 402,666, which relates to methods for producing alkane acetates by oxidative esterification of olefins over oxide/borate catalyst systems. Rare earth oxides are the catalysts in U.S. patent application Ser. No. 402,662. All related applications were filed on July 28, 1982.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The invention is related to a process for the production of alkane acetates by the oxidative esterification of olefins, and is particularly related to such a process conducted in the presence of a carboxylate ion source and a catalyst containing metal oxide.

2. Description of Relevant Methods

The production of ethylene oxide from ethylene has long been known. However, there has been a less successful search for a similar process for producing propylene oxide directly from propylene in an economic manner. The same processes which produced ethylene oxide cannot be adapted to the production of propylene oxide.

As a result, a number of different schemes to produce propylene oxide from propylene or to produce an intermediate to propylene oxide from propylene have been proposed. Initially the research effort seemed to be directed to producing an olefin oxide directly from the olefin in the presence or absence of a solvent. U.S. Pat. No. 2,649,463 describes the production of a coordination complex created by the reaction of an olefin with a metal halide where the metal is copper, platinum, palladium, iridium, aluminum, zinc, silver, mercury or antimony. This coordination complex is further reacted with oxygen at a high temperature to produce the olefin oxide plus oxygen-containing metal halides. Hawkins, et al. in an article entitled, "Autoxidation of Olefins," in the Journal of Applied Chemistry, Vol. 6, 1956, pgs 1 through 10, describes a process for the production of epoxides directly from olefins and molecular oxygen over magnesium oxide and/or cobalt naphthenate. The direct production of olefin oxides from a mono olefin and a saturated hydrocarbon with oxygen and water, organic acids or olefin oxide in low concentration is described in U.S. Pat. No. 2,780,634.

British Pat. No. 1,582,261 describes how propylene may be reacted with oxygen over a dinitrogen tetraoxide catalyst in a liquid medium of a chlorinated organic solvent to produce propylene oxide directly. Propylene oxide may also be prepared directly from propylene and oxygen over a catalyst system comprising a palladium cation plus a chloride anion in the presence of a phosphorous or arsenic ligand as revealed in U.S. Pat. No. 4,256,649.

Further, U.S. Pat. No. 2,784,202 outlines how propylene in a liquid hydrocarbon solvent, such as benzene, in the presence of oxygen and water, organic acids or propylene oxide in low concentration yield propylene oxide when heated at a temperature between 130° and 300° C. Propylene oxide is also proposed to be made directly from propylene in benzene in the presence of oxygen over a cobalt, copper, magnesium, vanadium or chromium catalyst where barium or lead is used as a promoter for the catalyst, according to U.S. Pat. No. 3,071,601. Brill, et al. in Journal of Organic Chemistry, Vol. 29, 1964, pgs 140-143, describes a process for passing olefins and oxygen, frequently in contact with or dissolved in benzene over various catalysts such as azobisisobutyronitrile, cadmium oxide, cobaltic acetylacetonate, magnesium oxide or methyl ethyl ketone peroxide to produce various oxidation products, including the desired epoxides. U.S. Pat. No. 3,132,156 reveals that ethylene, propylene or butylene oxide may be produced directly from ethane, propane or butane under very precise conditions. These conditions include a temperature of between 425° to 575° C., an oxygen volume percent of between 4 and 14, a contact time with the oxygen of between 0.07-1.5 seconds, a pressure of between 20 to 150 psig and constant concentrations of reactants. Epoxides may also be produced from olefins and oxygen which are in an inert reaction medium when they are brought in contact with a rhenium catalyst and 0.05 to 15 weight percent of a reaction modifier comprised of an alkyl aryl or cyclo alkyl cyanide, pyridine or quinoline in accordance with the invention described in U.S. Pat. No. 3,316,279.

Other schemes for producing olefin oxides from olefins and oxygen by means of a solvent or liquid reaction medium include the following. U.S. Pat. No. 3,153,058 employs polyacyl esters of polyhydroxy alkanes, polyhydroxy cycloalkanes, polyglycols or mixtures thereof as the solvent. Materials selected from saturated aliphatic, alicyclic and aromatic nitriles and mixtures thereof form the solvent in U.S. Pat. No. 3,210,380. Boric acid esters form the liquid reaction medium in U.S. Pat. No. 3,210,381. U.S. Pat. No. 3,228,967 uses major amounts of acetone as the solvent. Carbonic acid esters are employed in U.S. Pat. No. 3,228,968, and at least 25 percent by weight of certain ketones serves as the reaction medium in U.S. Pat. No. 3,232,957. Halogenated benzenes serve as the solvent in U.S. Pat. No. 3,238,229 while benzoic acid esters are employed in a similar reaction described in U.S. Pat. No. 3,281,433. Olefin oxides may be prepared directly from olefins and oxygen over a hydrocarbon soluble, phosphorous molybdenum-hydroxy compound catalyst according to the disclosure in U.S. Pat. No. 3,856,826. The approach of making epoxides directly has never been commercially feasible because all of the methods explored gave low yields of epoxides.

At this point in the history of this research, the emphasis seems to shift from making the olefin oxides directly to making an intermediate which could be converted to the olefin oxides by a second step. For example, U.S. Pat. No. 2,497,408 suggests the production of propylene glycol diacetate from propylene, oxygen and acetic acid over a metal acetate catalyst in which the metal is lead or iron in combination with an alkali earth metal acetate. Another example of this latter approach is U.S. Pat. No. 3,403,175 where olefins in oxygen are reacted in the presence of a reaction medium consisting of carboxylic acid and anhydrides with no catalyst to produce glycol diesters. Acyloxy compounds, which are intermediates to olefin epoxides, may be produced by the reaction of olefins with the metal salt of a carboxylic acid in an aqueous solution if electric current is passed through the solution, according to the method of U.S. Pat. No. 3,453,189. U.S. Pat. No. 3,479,395 reveals that olefins in oxygen may be converted to glycols and glycol acetates by being brought into contact with a solution comprising tellurium dioxide, an alkali metal halide and a redox agent dissolved in a solvent of certain specifications (water, acetic acid, dioxane, dialkyl formamides or dialkyl sulfoxides).

Further examples of the approach to making intermediates to the epoxides include U.S. Pat. No. 3,542,857 where vicinal glycol monoesters and diesters may be made by passing olefins in oxygen in an alkanoic acid medium over cerium salts. A method for making glycol esters from olefins and oxygen in a carboxylic acid medium over tellurium and an appropriate form of bromine is revealed in U.S. Pat. No. 3,668,239. British Pat. No. 1,278,353 teaches that non-vicinal glycols may be reacted with carbon monoxide over a rhodium or iridium catalyst together with a halogen promoter to produce dicarboxylic acids which are precursors to diesters which are intermediates to the epoxides. Further, British Pat. No. 1,326,219 discloses that glycol esters may be produced from olefins and oxygen in the presence of at least one carboxylic acid when a halogen is employed as an anion and a metal cation is present which is selected from the group of tellurium, cerium, antimony, manganese, arsenic or cobalt. Other examples which reveal how esters may be made from olefins include U.S. Pat. No. 3,770,813 where an olefin with a chloro, hydroxy or lower alkanoyloxy substituent together with oxygen and a monobasic carboxylic acid may be reacted together over an iodide anion and a heavy metal cation of atomic numbers 21 to 30 and 48, and nitrogen-containing cations to give glycol esters. Olefins and oxygen may be reacted together over a catalyst system comprising a metal cation of tellurium, cerium, antimony, vanadium, gallium, arsenic, copper, selenium or silver with a bromine or chlorine anion to produce vicinal glycol esters which are later fractionated to give a residue with a boiling point higher than the vicinal glycol esters according to the disclosure in U.S. Pat. No. 3,789,065. The residue is then contacted with a carboxylic acid to yield additional vicinal glycol esters. British Pat. No. 1,353,814 describes the reaction of olefins and oxygen in a carboxylic acid in the liquid phase that contains at least 0.5 percent water over a catalyst system identical to that of the patent previously described to also yield vicinal glycol esters. Ethylene or propylene may be reacted with oxygen in a carboxylic acid over a catalyst system comprising a tellurium cation and a bromide anion or a selenium cation plus a chloride or bromide anion to produce vicinal glycol esters as revealed in U.S. Pat. No. 3,907,874.

Aliphatic hydrocarbon carboxylic acid esters of vicinal glycols which contain organic halogen impurities may be purified by passing them over aquobasic alkali metal compounds, aquobasic earth metal compounds or compounds (other than halides) of zinc, lead, cadmium, tin, mercury, silver, manganese, copper, nickel, cobalt, iron or chromium in accordance with the invention in British Pat. No. 1,410,834. German Auslegeschrift No. 2,430,022 describes a multi-step procedure for producing butane diols, which are precursors to butane oxide, from propylene, oxygen and acetic acid.

A system which has obtained a fair amount of commercial importance is described in U.S. Pat. No. 4,045,477 by which vicinal hydroxy esters and diesters are produced from olefins and oxygen over tellurium and an iodide source. Organic monoesters of vicinal glycols may also be produced from olefins, oxygen, water and a carboxylic acid over a system comprising an iodine compound (such as copper iodide, manganese iodide or cerium iodide), a copper compound, and an activated ion taken from the group of manganese, cerium, alkali metals, alkali earth metals, nitric compounds or mixtures thereof, according to the invention in U.S. Pat. No. 4,061,868. U.S. Pat. No. 4,069,381 reveals how glycol monoesters may be made from olefins, oxygen and carboxylic acids over a catalyst system where the cation is zirconium, niobium molybdenum, hafnium, tantalum, tungsten or rhenium where the anion is a halide in the presence of lithium, sodium, potassium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, aluminum or silver.

Some of the more recent patents in this field include the following. Esters may be produced from olefins in an acid plus oxygen over a tin or cerium catalyst in the presence of iodide as revealed by U.S. Pat. No. 4,154,957. Saturated vicinal esters may be produced from olefins, carboxylic acids and oxygen in the presence of a boron-containing catalyst according to the invention of U.S. Pat. No. 4,220,800. U.S. Pat. No. 4,221,916 teaches that olefins, carboxylic acids and oxygen when reacted together over a vanadium oxide or ruthenium oxide-containing catalyst can also produce saturated vicinal esters. U.S. Pat. No. 4,238,624 discloses a procedure by which ethylene, oxygen and a lower alkanoic acid are reacted together over an iodine source in a bismuth stabilized tellurium oxide catalyst on a carbon support to give ethylene glycol mono- and dialkanoates.

Further, alkylene glycol dicarboxalates may be made from carboxylic acid esters of monohydric or polyhydric short chain alcohols and olefins and oxygen over a catalyst system comprising tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic or cobalt, plus a halogen anion and a hydrolyzing agent in addition to water as taught by U.S. Pat. No. 4,239,911.

Methods also exist for converting the ester intermediates into the epoxides. For example, U.S. Pat. No. 4,012,423 describes how vicinal hydroxy esters may be reacted over group I, II and IIIA basic metal carboxylates, being the preferred catalyst (sodium, potassium, lithium, calcium or barium, etc.), or group I, II and IIIA basic metal simple oxides and complex oxides and organic bases (such as borates, phosphates, oxides and carboxylates, particularly sodium borate, nickel oxide, etc.) to give epoxides. Another method is described in U.S. Pat. No. 4,158,008 whereby propylene glycol monoesters in the presence of a high boiling solvent is reacted over a base to produce propylene oxide. Propylene oxide may also be produced from propylene glycol with the removal of a water molecule over a weakly acidic carrier comprising a basic alkali metal salt of a low molecular weight carboxylic acid as taught by U.S. Pat. No. 4,226,780.

Of the numerous patents discussed so far, the ones considered to be most relevant to the invention at issue are U.S. Pat. Nos. 4,012,423; 4,069,381 and 4,221,916, all of which have been discussed.

Despite all of the investigative routes described so far and the ones that have been devised which have not been described, there is still a need for an efficient method for making propylene oxide from propylene, in addition to making the alkylene oxides from other olefins, which does not involve a highly corrosive or highly expensive catalyst system.

SUMMARY OF THE INVENTION

The invention concerns a process for the production of alkane acetates comprising reacting an olefin or a mixture of olefins with oxygen and a carboxylate ion source, in the presence of an oxide catalyst selected from the group of oxide catalysts consisting of niobium oxide, iron oxide and bismuth oxide.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

Alkane hydroxy acetates and diacetates, also called glycol monoesters or diesters or vicinal diesters, may be prepared by the oxygen or air oxidation of olefins in a solvent capable of generating a carboxylate ion in the presence of a metal oxide catalyst. The diacetates may be converted to epoxides or glycols using methods known in the art, some of which have been outlined previously. Both the epoxides and the glycols are of interest in the manufacture of important high volume products, including urethane polyols, gasoline additives, and heat transfer fluids.

According to the method of this invention, the olefin feedstocks may consist of any mono olefin having the double bond located anywhere within the molecule and mixtures of such olefins. The olefin may be an alpha or an internal olefin. Specific examples of suitable feedstocks include, but are not limited by, the following list: propylene, 1-butene, 2-butene, 1-pentene, 2-pentene, 1-hexene, 2-hexene, 3-hexene, heptenes, octenes, nonenes, decenes, undecenes, dodecenes, tridecenes such as 6-tridecene, tetradecenes such as 7-tetradecene, pentadecenes, hexadecenes, etc., and mixtures thereof. Preferably, the olefin has 3 to 16 carbon atoms. Propylene is an especially preferred olefin.

Of course, molecular oxygen in a pure form or air is an essential co-reactant for the method of this invention.

The co-reactant and solvent must be a compound capable of generating a carboxylate ion when it serves as a solvent. These compounds may be generally described as carboxylic acids or anhydrides. They may include materials such as acetic acid, acetic anhydride, carboxylic acids, although acetic acid and acetic anhydride are the preferred solvents/co-reactants. Acetic acid is the preferred co-reactant of this invention.

Catalysts found to be useful in the method of this invention include metal oxides. Oxide compounds are novel for the catalysis of olefins to olefin acetates and diacetates (also called esters and diesters) never having been previously discovered. The preferred oxides are niobium oxide, iron oxide and bismuth oxide. The especially preferred iron oxide is iron (II, III) oxide (Fe₃ O₄). These catalysts are much less corrosive than many of those used in other methods, especially the halide systems. Also, much smaller catalyst levels may be used. They are also less expensive than many of the catalyst systems proposed. These catalysts may be used in mixtures with each other or with other catalysts.

Not all metal oxides work well as catalysts in the instant method. For example, it will be shown that vanadium oxide and molybdenum oxide are poor catalysts for the reaction of this invention.

The reaction conditions under which the method of this invention may be conducted include a temperature range of from 100° to 250° C. A preferred range is from 120° to 220° C. The pressure may be one atmosphere or higher. These conditions are much milder than many of those in the prior art discussed earlier.

An initiator may be optionally used to provide an initial source of free radicals which will help start the oxidation as well as prevent a possible build-up of peroxides which would be dangerous. Readily oxidizable compounds such as aldehydes are suitable initiators with heptaldehyde being the preferred initiator. Usually a few drops are enough to be effective, i.e. quantities on the order of 1.0 ml. Peroxides and azo compounds are also used as initiators.

The invention will be further illustrated by the following examples which are not intended to limit the scope of the invention except as noted.

EXAMPLES

The examples followed the procedure described below. Example 1 employed the vanadium oxide catalyst of U.S. Pat. No. 4,221,916 while Example 2 used the iron (II, III) oxide catalyst of this invention. Examples 3 and 4 employed no catalyst, and the resultant conversions are poor. Examples 1, 5 and 6 demonstrate that poor conversions and poor selectivities (less than 70 weight percent selectivity) may occur if the metal oxide is other than those of this invention. Examples 7 through 11 demonstrate the usefulness of bismuth oxide and niobium oxide in the method of this invention.

A 1-liter 316 stainless steel glass-lined autoclave equipped 71 a magnetic stirrer was charged with 300 ml of glacial acetic acid and catalyst. Also present was 1.00 ml of heptaldehyde. The autoclave was sealed, 42 g of propylene was pressured in, and the mixture was heated to the desired temperature. Oxygen was added slowly to a pressure 50 -100 psi higher than autogeneous pressure. The pressure was maintained by addition of oxygen from time to time (after each addition of oxygen there was a small exotherm) for the desired reaction time. The reaction mixture was then cooled to room temperature, the reactor vented and the contents analyzed by vapor phase chromatography. The results are shown in Table I.

                  TABLE I                                                          ______________________________________                                              Catalyst       Temp. Time  Approx. Esters wt.                             Ex.  ID       (g)   (°C.)                                                                         (Hr)  Conv. (%)                                                                              Selectivity                            ______________________________________                                         1    V.sub.2 O.sub.5                                                                         1.0   160   5     10      63.4                                   2    Fe.sub.3 O.sub.4                                                                        1.0   160   5     9       67.0                                   3    None     --    160   5     4       83.2                                   4*   None     --    160   5     4       ˜0                               5    MoO.sub.2                                                                               0.5   160   5     <1      --                                     6    MoO.sub.2                                                                               1.0   160   5     <1      --                                     7    Bi.sub.2 O.sub.3                                                                        1.0   160   5     7       82.3                                   8    Bi.sub.2 O.sub.3                                                                        1.0   170   5     21      72.5                                   9    Bi.sub.2 O.sub.3                                                                        1.0   180   5     22      71.5                                   10   Nb.sub.2 O.sub.5                                                                        1.0   180   5     8       80.2                                   11   Nb.sub.2 O.sub.5                                                                        1.0   170   5     17      79.3                                   ______________________________________                                          *No heptaldehyde initiator was present.                                  

It may be seen that the conversion and selectivity of Example 2 using the iron oxide of this invention are comparable to those obtained in Example 1 which employed the vanadium oxide catalyst of U.S. Pat. No. 4,221,916.

Many modifications may be made in the method of this invention by those skilled in the art to maximize the yields of the desirable acetates without departing from the spirit and scope of the invention which is defined only by the appended claims. For example, one skilled in the art could determine an exact combination of metal oxide catalyst amounts, temperatures, feedstocks and modes of addition to optimize the yield. 

We claim:
 1. An improved process for the production of alkane hydroxy acetates and diacetates by reacting an olefin or a mixture of olefins with oxygen and a carboxylate ion source selected from the group consisting of acetic acid and acetic anhydride wherein the improvement consists essentially of conducting the reaction in the presence of an oxide catalyst selected from the group of oxide catalysts consisting of niobium oxide, iron oxide and bismuth oxide.
 2. The process of claim 1 in which the reaction is conducted at a temperature in the range of 120° to 220° C.
 3. The process of claim 1 in which the olefins have 3 to 16 carbon atoms.
 4. The process of claim 1 in which the olefin is propylene.
 5. The process of claim 1 in which the iron oxide catalyst is iron (II, III) oxide.
 6. The process of claim 1 in which the carboxylate ion source is acetic acid.
 7. An improved process for the production of alkane hydroxy acetates and diacetates by reacting an olefin or a mixture of olefins where each molecule has 3 to 6 carbon atoms, with oxygen and a carboxylate ion source selected from the group consisting of acetic acid and acetic anhydride at a temperature in the range of 120° to 220° C., wherein the improvement consists essentially of conducting the reaction in the presence of an oxide catalyst selected from the group of oxide catalysts consisting of niobium oxide, iron oxide and bismuth oxide.
 8. The process of claim 7 in which the iron oxide catalyst is iron (II, III) oxide.
 9. The process of claim 7 in which the carboxylate ion source is acetic acid.
 10. The process of claims 7, 8 or 9 in which the olefin is propylene. 